<?xml version="1.0" encoding="ISO-8859-1"?><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance">
<front>
<journal-meta>
<journal-id>0872-1904</journal-id>
<journal-title><![CDATA[Portugaliae Electrochimica Acta]]></journal-title>
<abbrev-journal-title><![CDATA[Port. Electrochim. Acta]]></abbrev-journal-title>
<issn>0872-1904</issn>
<publisher>
<publisher-name><![CDATA[Sociedade Portuguesa de Electroquímica]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0872-19042006000300005</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[A modified electrodialytic cell to recover heavy metals from wastewater]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Abo-Ghander]]></surname>
<given-names><![CDATA[N.S.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Rahman]]></surname>
<given-names><![CDATA[S.U.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Zaidi]]></surname>
<given-names><![CDATA[S.M.J.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,King Fahd University of Petroleum & Minerals Chemical Engineering Department Electrochemical Research Group]]></institution>
<addr-line><![CDATA[Dhahran ]]></addr-line>
<country>Saudi Arabia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2006</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2006</year>
</pub-date>
<volume>24</volume>
<numero>3</numero>
<fpage>367</fpage>
<lpage>376</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_arttext&amp;pid=S0872-19042006000300005&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_abstract&amp;pid=S0872-19042006000300005&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_pdf&amp;pid=S0872-19042006000300005&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[A modified electrodialytic cell integrates electrodialysis and reduction of metal ions. The cell is able to recover metallic copper from wastewater containing 1000 ppm cupric ions and bring the concentration down to about 1 ppm. The kinetic data of decreasing copper ion concentration fit well in first order kinetics and allow calculation of the over all reaction rate constant. Effect of several parameters, namely, width of wastewater compartment, applied potential and concentration of anolyte and catholyte solution; on the over all reaction rate constant and specific energy consumption were studied. The best combination of parameters results in an overall rate constant of 7.84 × 10-4 sec-1 and specific energy consumption of 48.18 kW-h/kg copper.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[electrodialysis]]></kwd>
<kwd lng="en"><![CDATA[electrolysis]]></kwd>
<kwd lng="en"><![CDATA[copper ions]]></kwd>
<kwd lng="en"><![CDATA[wastewater]]></kwd>
<kwd lng="en"><![CDATA[water treatment]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="center"><b>A modified electrodialytic cell to recover heavy metals from    wastewater</b></p>     <p align="center"><b>N.S. Abo-Ghander, S.U. Rahman</b><a href="#1">*</a><a name="top1"></a>,    <b >S.M.J. Zaidi</b></p>     <p align="center"><i>Electrochemical Research Group, Chemical Engineering Department,    King Fahd University of Petroleum &amp; Minerals, Dhahran-31261, </i><i>Saudi    Arabia</i></p>     <p align="center">&nbsp;</p>          <p><b>Abstract</b></p>      <p align="justify">A modified electrodialytic cell integrates electrodialysis    and reduction of metal ions. The cell is able to recover metallic copper from    wastewater containing 1000 ppm cupric ions and bring the concentration down    to about 1 ppm. The kinetic data of decreasing copper ion concentration fit    well in first order kinetics and allow calculation of the over all reaction    rate constant. Effect of several parameters, namely, width of wastewater compartment,    applied potential and concentration of anolyte and catholyte solution; on the    over all reaction rate constant and specific energy consumption were studied.    The best combination of parameters results in an overall rate constant of 7.84    × 10<sup>-4</sup> sec<sup>-1</sup> and specific energy consumption of 48.18    kW-h/kg copper.</p>        <p><b><i>Keywords: </i></b>electrodialysis, electrolysis, copper ions, wastewater,    water treatment.</i></b></p>     <p>&nbsp;</p>        <p>Texto disponível em PDF</p>     <p>Full text only in PDF format</p>     ]]></body>
<body><![CDATA[<p>&nbsp;</p>     <p>&nbsp;</p>        <p><b>References</b></p>         <!-- ref --><p> 1. U. S. Environmental Protection Agency Regulation. Identification and listings    of hazardous wastes, Guideline 40, CFR 413, 1992.&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000016&pid=S0872-1904200600030000500001&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --><p>2. L. J. J. Janssen, L. Koene, The role of electrochemistry and electrochemical    technology in environmental protection, <I>Chem. Eng. Journal </I>85 (2002)    137-146.</p>         <p> 3. L. Koene, L.J.J. Janssen, Removal of nickel from industrial process liquids,    <I>Electrochimica Acta </I>47 (2001) 695-703.</p>         <p>4. K. Juttner, U. Galla, H. Schiemder, Electrochemical approaches to environmental    problem in the process industry, <I>Electrochimica Acta</I> 45 (2000) 2575-2594.</p>        <p>5. R. P. Tison, Copper recovery using a tumbled-bed electrochemical reactor,    <I>J. Electrochem</I>. 128 (1981) 317-322.</p>       <p>      6. M. Fleishmann, J.W. Oldfield, L. Tennakkoon, Electrochemical removal of      copper ions by use of fluidized bed electrode, <I>J. Appl.      Electrochem</I>.  1 (1971a) 103.</p>         <p> 7. D. N. Bennion, J. Newman, Electrochemical removal of copper ions from very    dilute solutions, <I>J. Appl. Electrochem</I>. 2 (1972) 113-122.</p>         ]]></body>
<body><![CDATA[<p>8. P. M. Robertson, O. Dossenbach, Stirring by gas introduction and its application    in the electroplating industry, <I>Oberflaeche-Surf</I>. 22(9) (1981) 282-287.</p>         <p>9. F. S. Holland, The development of eco-cell process, <I>Chem. Ind.</I> July    (1978) 453-458.</p>        <p>      10. M. Fleishmann, C.J.H. King, J.W. Oldfield, R.E. Plimley, C.L.K. Tennakkoon, Improvement in and relating to electrochemical      cells. <I>Br. Pat.</I> 1419246. (1971b).</p>        <p> 11. M. Fleishmann, R.E.W.  Jansson, R.J. Marshall,      Improvement in and relating to electrochemical cells. <I>Br. Pat. 1522872.</I> (1976).</p>         <p>12. R. P. Tison, B. Howie, Copper recovery from dilute solutions using a barrel    plater, <I>Plat. Surf. Fin.</I> 71(9) (1984) 54-56.</p>         <p>13. C. D. Zhou, D.T. Chin, Copper recovery and cyanide destruction with a plating    barrel cathode and a packed-bed anode, <I>Plat. Surf. Fin.</I>  80(6) (1993)    69-77.</a></p>         <p> 14. C. D. Zhou, D.T. Chin, Continuous electrolytic treatment of complex metal    cyanides with a rotating barrel plater as the cathode and a packed-bed as the    anode, <I>Plat. Surf. Fin.</I>  81 (6) (1994) 70-78.</p>     <p > 15. A. A. Al-Shammari, S.U. Rahman, D.T. Chin, Copper recovery from wastewater    using an electrochemical rotating barrel reactor, <I>J. Appl. Electrochem.</I>    <b> </b>34 (2004) 447-453.</p>        <p> 16. T. Seto, L. Ehara, R. Komori, A. Yamaguchi, T. Miwa, Seawater desalination      by electrodialysis, <I>Desalination</I> 25<b> </b>(1978) 1-7.</p>         <p >17. S. Resbeut, G. Pourcelly, R. Sandeaux, C. Gavach,    Electromembrane processes for waste treatment: electrodialysis applied to the    demineralization of phenylalnine solutions, <I>Desalination</I>  120 (1998) 235-245.</p>         ]]></body>
<body><![CDATA[<p> 18. A. J. Chaudhary, J.D. Donaldson, S.M. Grimes, N.G. Yasri, Separation of    nickel from cobalt using elecrodialysis in the presence of EDTA, <I>J. Appl.    Electrochem.</I> 30 (2000) 439-445.</p>        <p>19. H. Grib, D. Belhocine, H. Lounici, H. Pauss, N. Mameri, Desalting of phenylalanine      solutions by electrolysis with ion-exchange membrane, <I>J. Appl. Electrochem.</I> <b> </b>30      (2000) 259-262.</p>        <p>20. M. Davis, Use advanced methods to treat wastewater, <I>Hydrocarbon      Proc.</I>  73 (1994) 43-46.</p>         <p> 21. K. K. Chin, S.L. Ong,  Water conservation through reclamation of sewage    for reuse. Proceedings of 22<sup>nd</sup> Annual Conf. Integrated Water Resource    Planning for 21<sup>st</sup> Century, Cambridge, USA. (1995) pp 73-76.</p>         <p> 22. A. S. Bal, A.N. Vaidya, Application of membrane technology in wastewater    management, <I>Chem. Eng. World </I>33 (1998) 5.</p>         <p>23. Tokuyama Corp. Brochure, Neosepta Ion-exchange membranes, South Korea    (1999).</p>      <p>&nbsp;</p>     <p><a href="#top1">*</a><a name="1"></a>Corresponding author. E-mail address:    <a href="mailto:srahman@kfupm.edu.sa">srahman@kfupm.edu.sa</a></p>     <p>&nbsp;</p>       ]]></body><back>
<ref-list>
<ref id="B1">
<nlm-citation citation-type="book">
<collab>U. S. Environmental Protection Agency Regulation</collab>
<source><![CDATA[Identification and listings of hazardous wastes]]></source>
<year>1992</year>
<volume>413</volume>
<publisher-name><![CDATA[Guideline 40]]></publisher-name>
</nlm-citation>
</ref>
</ref-list>
</back>
</article>
